US4316878A - Method for the combustive treatment of waste fluids containing nitrogen compounds - Google Patents

Method for the combustive treatment of waste fluids containing nitrogen compounds Download PDF

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Publication number
US4316878A
US4316878A US06/117,507 US11750780A US4316878A US 4316878 A US4316878 A US 4316878A US 11750780 A US11750780 A US 11750780A US 4316878 A US4316878 A US 4316878A
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combustion chamber
combustion
primary
waste
temperature
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Expired - Lifetime
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US06/117,507
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English (en)
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Mikio Akune
Yoshiaki Kinoshita
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Tsukishima Kankyo Engineering Ltd
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Nittetsu Chemical Engineering Co Ltd
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • F23G5/165—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber arranged at a different level
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/008—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for liquid waste
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
    • F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel

Definitions

  • This invention relates to a method for the combustive treatment of a waste fluid, such as an exhaust gas or spent liquor, which contains compounds generating nitrogren oxides upon combustion in the presence of air.
  • the NO x Large amounts of nitrogen oxides, the NO x , are produced when burning waste materials containing nitrogen compounds, causing a problem of environmental pollution.
  • the nitrogen compounds have no nitrogen-hydrogen bonds such as nitro, nitroso, nitrate, cyan, isocyanate and cyanate compounds, they are easily decomposed or oxidized within wide ranges of temperature and oxygen concentrations to generate nitrogen oxides. In view of preventing air pollution which has now become a big social problem, therefore, it is highly desirable to inhibit discharge of nitrogen oxides from combustion units.
  • the present invention provides a method for combusting a waste fluid containing nitrogen compounds in an incinerator having cylindrical, coaxially aligned primary and secondary combustion chambers connected in series by a connecting member having a throat portion, and a burner located in the primary combustion chamber and adapted for burning combustible materials contained in the waste fluid.
  • the steps involved in the method include feeding the waste fluid and, if necessary, an auxiliary fuel to the primary combustion chamber to combust same at a temperature of at least 1200° C. while injecting air thereinto at a velocity and in a direction tangential to the inner periphery of the primary combustion chamber to establish a vortex therein.
  • the thus formed whirling combustion gas containing large amounts of nitrogen oxides is then caused to pass at a high velocity through the throat portion into which a fluid containing compounds having nitrogen-hydrogen bonds, such as amines and ammonia, is injected for uniform mixing therewith.
  • the resulting mixture is then introduced into the secondary combustion chamber for combustion at a temperature of between 850° and 1150° C. while maintaining the oxygen concentration at the exit of the secondary combustion chamber not greater than 5% by volume. Under such combustion conditions in the secondary chamber, the generation of nitrogen oxides is substantially prevented and, moreover, the nitrogen oxides produced in the combustion in the primary chamber and introduced into the secondary chamber are converted into molecular nitrogen by reduction with the compounds containing nitrogen-hydrogen bonds.
  • a part of the waste fluid can be used as at least a part of the fluid which is injected into the throat portion. Further, all of such a waste fluid can be fed to the throat portion for combustion in the secondary combustion chamber. In this case, it is necessary to feed an auxiliary fuel to the burner of the primary combustion chamber in order to effect the combustion of the waste fluid in the secondary chamber.
  • the waste fluid When the nitrogen compounds in the waste fluid are of the type which generate nitrogen oxides upon combustion at a temperature of 850° to 1150° C. in an atmosphere of a residual oxygen concentration of not greater than 5% by volume, the waste fluid should be combusted in the primary combustion chamber.
  • the waste fluid and the fluid to be injected into the throat portion can contain organic materials as well. If the content of the organic materials is high, cooling water is fed to the throat portion so as to maintain the combustion temperature in the secondary combustion chamber within the range of between 850° and 1150° C.
  • the cooling water too can contain organic materials.
  • an object of the present invention to provide a method by which waste gases or liquids containing nitrogen compounds can be combusted with incinerator in a high efficiency while minimizing the discharge of nitrogen oxides therefrom.
  • Another object of this invention is to provide a method for the combustive treatment of such a waste fluid using a small size incinerator.
  • FIGURE is a cross-sectional, elevational view diagrammatically showing the incinerator system used for carrying out the method of this invention.
  • the incinerator system has a cylindrical primary combustion chamber 1 which is connected in series to and coaxially aligned, preferably vertically, with a cylindrical secondary combustion chamber 2 by means of a joining member 3.
  • the primary and secondary combustion chambers include first and second housings 4 and 5, respectively, each of which is lined throughout with a suitable refractory material (not shown).
  • the joining member 3 is also lined with a suitable refractory and is shaped so as to define within it a throat portion 6.
  • the joining member 3 is of a venturi or an orifice type and widens toward both its upper and lower ends.
  • a burner 7 is located in the primary combustion chamber 1, to which a waste fluid, air and, if necessary, an auxiliary fuel are supplied through lines 8, 9 and 10, respectively, for combustion in the chamber 1.
  • a fluid injection nozzle 11 extends through the center of the end wall of the first housing 4 and is so configured as to cause the fluid introduced from a line 12 to be injected toward the center of the throat portion 6.
  • a mantle 13 formed of a refractory material surrounds the nozzle 11 for protecting it from the impingement of the high temperature combustion gas.
  • a space 14 defined between the nozzle 11 and the mantle 13 serves as a passage for air introduced from a line 15 for thermal protection of the nozzle.
  • Means, preferably two or more angularly equally spaced nozzles 16 are provided at the periphery of the throat portion 6, from which cooling water fed from a line 17 is introduced into the throat portion 6.
  • the waste liquid is fed through the line 8 to the burner 7 where it is mixed with air supplied from the line 9 for injection into the primary combustion chamber 1.
  • the combustion in the primary combustion chamber 1 is effected at a temperature of at least 1200° C., preferably between 1250° and 1500° C.
  • a liquid or gas auxiliary fuel such as L.P.G. (liquified petroleum gas) around a fuel oil, e.g. kerosene and Bunker C, is fed through the line 10 in an amount sufficient to effect the combustion in the primary combustion chamber 1 at a temperature of at least 1200° C.
  • the auxiliary fuel is also fed to the primary combustion chamber through the burner 7 when a desirable combustion temperature in the second combustion chamber 2 is not obtained.
  • the air and, preferably the waste liquid and auxiliary fuel too, are injected at a velocity and in a direction tangential to the inner periphery of the primary combustion chamber 1.
  • the nitrogen oxides-containing combustion gas is caused to whirl in a vortex pattern along the inner wall of the first housing 4 and the flow velocity thereof becomes higher as it flows towards the throat portion 6.
  • the high temperature gas produced in the primary combustion chamber 1 serves as an igniter to effect the combustion in the secondary combustion chamber 2.
  • the burning out of combustible materials contained in the mixture is effected together by the reduction of nitrogen oxides with the compounds having nitrogen-hydrogen bonds.
  • the fluid containing compounds having nitrogen-hydrogen bonds is introduced into the throat portion 6 in an amount such that the content of nitrogen oxides in the waste combustion gas exhausted from the secondary combustion chamber 2 is reduced to a predetermined value.
  • the feed amount of the fluid is preferably such that the molar ratio of the nitrogen-hydrogen bonds to the oxygen atoms of the nitrogen oxides produced in the primary combustion chamber 1 is at least 1.5, preferably at least 2.0.
  • the fluid to be injected through the nozzle 11 into the throat portion 6 can contain organic materials. Since organic materials such as hydrocarbons may act as reducing agents for nitrogen oxides, their presence in the fluid is preferable. When a waste liquid or gas containing compounds having nitrogen-hydrogen bonds is available, the use thereof as the fluid to be injected into the throat portion 6 is desirable.
  • cooling water is supplied from the nozzles 16 into the throat portion 6 to control the temperature within the secondary combustion chamber 2 to within the range of between 850° and 1150° C.
  • the oxygen content in the combustion system in the secondary combustion chamber 2 is another important factor for minimizing the content of nitrogen oxides in the gas exhausted from the secondary combustion chamber 2.
  • Good results can be obtained by maintaining the residual oxygen content in the exhaust gas from the secondary combustion chamber 2 at not greater than 5% by volume, preferably at not greater than 3% by volume. Since too low an oxygen content tends to lead to an increase in concentration of carbon monoxide and hydrogen gas and to the formation of soot in the exhaust gas, it is preferred that the residual oxygen content be not lower than 0.5% by volume.
  • the control of the residual oxygen content can be done by adjustment of the feed amount of air supplied from the line 9 and 15.
  • the waste liquid to be treated contains compounds having nitrogen-hydrogen bonds and does not yield nitrogen oxides upon combustion under the conditions adopted in the secondary combustion chamber 2
  • a portion thereof can be subjected to the combustive treatment in the primary combustion chamber 1 while the other portion may be used as at least a part of the fluid injected from the nozzle 11.
  • the waste liquid may be treated only in the second combustion by introducing it through the nozzle 11 while introducing an auxiliary fuel through the line 10 in an amount sufficient to provide necessary temperatures in the primary and secondary combustion chambers.
  • the nitrogen oxides produced by the combustion of the auxiliary fuel are converted into nitrogen gas by reduction with the waste liquid in the secondary combustion chamber 2.
  • the exhaust gas from the secondary combustion chamber 2 can be introduced into a tertiary combustion chamber 18 for further combustion treatment thereof. This is desirable especially when the waste combustion gas from the secondary combustion chamber 2 contains carbon monoxide.
  • the combustion in the tertiary combustion chamber 18 is effected at a temperature not exceeding 1000° C.
  • the tertiary combustion chamber is provided contiguous to the second combustion chamber 2 and has an air injection nozzle means 19 located downstream the outlet of the secondary combustion chamber 2.
  • the waste combustion gas from the secondary combustion chamber 2 or tertiary combustion chamber 18 may be introduced through a pipe 21 into a quench tank 22 where it is brought into contact with quenching water, thereby to cool the waste combustion gas and to collect ashes contained therein.
  • the vapor laden gas emitted from the tank 22 is discharged to the air or introduced into a heat exchanger, mist separator or the like through a duct 23.
  • the waste combustion gas from the chamber 2 or 18 may be introduced into a heat exchanger such as waste heat boiler for recovering the heat thereof.
  • the waste combustion gas contains molten ashes, it is introduced into the boiler after cooling to a temperature below the melting temperature of the ashes.
  • Such ashes are generally produced when the fluid injected from the nozzle 11 or the cooling water supplied from the nozzles 16 contains alkali metal salts and other metal salts.
  • a waste liquid containing 70 wt % of organic materials (17 wt % of aniline and 53 wt % of other organic compounds) and 30 wt % of water was treated at a rate of 500 Kg/hour in accordance with the method of this invention using the incinerator system shown in the FIGURE.
  • the inner diameters of the primary combustion chamber 1, the throat portion 6 and the secondary combustion chamber 2 were 900, 300 and 1300 mm, respectively.
  • the lengths of the chambers 1 and 2 were 1300 and 3500 mm, respectively.
  • the calorific value of the organic materials was 6000 Kcal/Kg.
  • 250 Kg/hour of the waste liquid and 50 Kg/hour of kerosene were continously fed through the lines 8 and 10 to the burner 7 which opened into the primary combustion chamber 1 tangentially to the inner periphery thereof.
  • the waste liquid and the kerosene were injected from the burner 7 using 2700 Nm 3 /hour of air, supplied thereto through the line 9, into the primary combustion chamber 1 for complete combustion at a temperature of 1350° C. and a residual oxygen concentration of about 9% by volume.
  • a vortex was established in the chamber 1.
  • the content of nitrogen oxides in the combustion gas at the outlet portion of the primary combustion chamber 1 was 1200 ppm.
  • waste water containing 6 wt % of organic materials (calorific value 4000 Kcal/Kg), 4 wt % of sodium chloride and 90 wt % of water at a rate of 1200 Kg/hour from three nozzles 16.
  • the whirling combustion gas produced in the primary combustion chamber 1 and containing nitrogen oxides was vigorously mixed with the waste liquid and the waste water during its passage through the throat portion 6 and the mixture was admitted into the secondary combustion chamber 2 and burnt there at a temperature of 1000° C. with a residual oxygen concentration of 2% by volume.
  • the concentration of nitrogen oxides in the gas exhausted from the secondary combustion chamber 2 was reduced to 80 ppm.
  • the gas was introduced into the tertiary combustion chamber 18 for further treatment. Air was fed through the line 20 and four nozzles 19 to the tertiary combustion chamber 18 at a rate of 300 Nm 3 /hour. The combustion in the chamber 18 was effected at a temperature of 900° C. No increase in nitrogen oxides concentration in the exhaust gas from the chamber 18 was found. The exhaust gas was then introduced into the quenching vessel 22 through the tube 21 for cooling same and for recovering sodium chloride contained therein. The combustion gas was cooled to about 90° C. upon contact with the liquid in the vessel 22 and was then discharged into the air.

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Incineration Of Waste (AREA)
  • Combustion Of Fluid Fuel (AREA)
  • Chimneys And Flues (AREA)
US06/117,507 1979-02-08 1980-02-01 Method for the combustive treatment of waste fluids containing nitrogen compounds Expired - Lifetime US4316878A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP1278779A JPS55105111A (en) 1979-02-08 1979-02-08 Process for combustion of fluid
JP54-12787 1979-02-08

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US (1) US4316878A (enrdf_load_stackoverflow)
JP (1) JPS55105111A (enrdf_load_stackoverflow)
DE (1) DE3004186A1 (enrdf_load_stackoverflow)
GB (1) GB2043854B (enrdf_load_stackoverflow)
NL (1) NL8000655A (enrdf_load_stackoverflow)

Cited By (23)

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US4499832A (en) * 1983-12-23 1985-02-19 Mcneil Roderick J Apparatus and method for material disposal
US4519993A (en) * 1982-02-16 1985-05-28 Mcgill Incorporated Process of conversion for disposal of chemically bound nitrogen in industrial waste gas streams
US4562778A (en) * 1983-05-20 1986-01-07 Rhone-Poulenc Chimie De Base High temperature reaction apparatus
US4584465A (en) * 1981-10-22 1986-04-22 Skf Steel Engineering Ab Method and apparatus for heating process air for industrial purposes
US4700637A (en) * 1981-11-27 1987-10-20 Combustion Engineering, Inc. Volume reduction of low-level radiation waste by incineration
US4702073A (en) * 1986-03-10 1987-10-27 Melconian Jerry O Variable residence time vortex combustor
US4819571A (en) * 1986-08-08 1989-04-11 Eli-Eco Logic Inc. Process for the destruction of organic waste material
US4934286A (en) * 1989-08-24 1990-06-19 Fowler Benjamin P Apparatus and method for the disposal of waste
US4954323A (en) * 1988-11-01 1990-09-04 The Standard Oil Company AOG incinerator NOx emission control via NH3 injection
US5050511A (en) * 1986-08-08 1991-09-24 655901 Ontario Inc. Process for the destruction of organic waste material
EP0773406A3 (en) * 1995-11-08 1997-12-10 Process Combustion Corporation Method to minimize chemically bound NOx in a combustion process
US5704557A (en) * 1995-03-06 1998-01-06 Eli Eco Logic Inc. Method and apparatus for treatment of organic waste material
US5817909A (en) * 1992-11-16 1998-10-06 Rhone-Poulenc Chimie Purification of waste/industrial effluents comprising organic/inorganic pollutants
US20090000530A1 (en) * 2007-03-02 2009-01-01 Fujita Manufacturing Co., Ltd Waste oil combustion apparatus
US20100077942A1 (en) * 2008-09-26 2010-04-01 Air Products And Chemicals, Inc. Oxy/fuel combustion system with little or no excess oxygen
US20120012038A1 (en) * 2010-07-19 2012-01-19 Dylan Smuts Dual Chamber Combustor
KR20160034399A (ko) * 2013-07-24 2016-03-29 에보니크 룀 게엠베하 아민 촉매 공정에서 촉매 수용액의 재순환 및 처분
WO2016055511A1 (en) * 2014-10-07 2016-04-14 Linde Aktiengesellschaft Incineration of waste
US20160159719A1 (en) * 2013-07-24 2016-06-09 Evonik Roehm Gmbh Method of regulating the water content in a continuous method for producing methacrolein
CN105722814A (zh) * 2013-12-12 2016-06-29 赢创罗姆有限公司 作为甲基丙烯醛合成中的共催化剂的烷基叔胺
CN106678839A (zh) * 2016-12-15 2017-05-17 南宁广发重工集团有限公司 高温空气预热式高温净化炉
CN111895427A (zh) * 2020-08-26 2020-11-06 江苏蓝创环保科技有限公司 超低氮氧化物排放的直接燃烧焚烧炉
CN112303648A (zh) * 2019-08-02 2021-02-02 中国石油化工股份有限公司 用于回收含固危险废物中金属元素的焚烧装置及其回收方法和应用

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US4499833A (en) * 1982-12-20 1985-02-19 Rockwell International Corporation Thermal conversion of wastes
JPS59164816A (ja) * 1983-03-10 1984-09-18 Nippon Kokan Kk <Nkk> ごみ焼却炉における燃焼排ガス中の窒素酸化物除去方法
DE59007204D1 (de) * 1989-07-19 1994-10-27 Siemens Ag Brennkammer zum Verbrennen zumindest teilweise brennbarer Stoffe.
US5216968A (en) * 1990-11-09 1993-06-08 Bayer Aktiengesellschaft Method of stabilizing a combustion process
JP3124871B2 (ja) * 1992-07-31 2001-01-15 ゼネラル・エレクトリック・カンパニイ ナトリウム含有廃棄物を破壊処理する方法及び装置
DE19540347A1 (de) * 1995-10-28 1997-04-30 Gutehoffnungshuette Man Hochtemperaturanlage zum Verbrennen von toxischen Pyrolysegasen und Pyrolysereststoffen
EP1143197B1 (en) * 1998-12-01 2017-03-29 Ebara Corporation Exhaust gas treating device
KR100405801B1 (ko) * 2000-05-01 2003-11-15 한국에너지기술연구원 액중배기식 폐액소각로 냉각조에서의 맥동억제 장치
KR100966116B1 (ko) 2008-07-18 2010-06-28 (주) 화성프랜트 암모니아가 함유된 폐가스의 소각 처리장치
CN104344408B (zh) * 2014-11-04 2016-09-14 宜兴市智博环境设备有限公司 含盐废液焚烧兼热能回收系统及工艺
CN105972605A (zh) * 2016-03-29 2016-09-28 东南大学 小型生活垃圾焚烧处理系统及焚烧处理方法
CN112303647B (zh) * 2019-08-02 2022-11-01 中国石油化工股份有限公司 用于回收含固危险废物中金属元素的单喷嘴焚烧装置、回收方法和应用
CN111271715B (zh) * 2020-02-27 2022-04-22 亚德（上海）环保系统有限公司 一种组合式低氮低能耗焚烧炉以及焚烧工艺
CN111322631B (zh) * 2020-03-13 2021-12-03 浙江鑫盛永磁科技有限公司 一种基于磁流体发电的燃烧室灰渣处理装置

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GB1121602A (en) 1964-12-23 1968-07-31 Stein Atkinson Strody Ltd Improvements in the production of gases
US3838193A (en) * 1971-03-13 1974-09-24 Kawasaki Heavy Ind Ltd Method of treating nitrogen oxide generating substances by combustion
DE2550635A1 (de) * 1974-11-11 1976-05-20 Mitsubishi Chem Ind Verfahren zur entfernung von stickstoffoxiden aus verbrennungsabgasen
US4080425A (en) * 1975-05-26 1978-03-21 Asahi Kasei Kogyo Kabushiki Kaisha Elimination of nitrogen oxides from exhaust gases with nitriles
JPS526142A (en) * 1975-07-04 1977-01-18 Babcock Hitachi Kk Gas heating method
US4115515A (en) * 1976-04-20 1978-09-19 Exxon Research And Engineering Company Method for reducing NOx emission to the atmosphere
US4154567A (en) * 1977-01-07 1979-05-15 Continental Carbon Company Method and apparatus for the combustion of waste gases
US4216060A (en) * 1978-05-10 1980-08-05 Mitsubishi Kasei Kogyo Kabushiki Kaisha Horizontal type coke ovens

Cited By (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4584465A (en) * 1981-10-22 1986-04-22 Skf Steel Engineering Ab Method and apparatus for heating process air for industrial purposes
US4700637A (en) * 1981-11-27 1987-10-20 Combustion Engineering, Inc. Volume reduction of low-level radiation waste by incineration
US4519993A (en) * 1982-02-16 1985-05-28 Mcgill Incorporated Process of conversion for disposal of chemically bound nitrogen in industrial waste gas streams
US4562778A (en) * 1983-05-20 1986-01-07 Rhone-Poulenc Chimie De Base High temperature reaction apparatus
US4499832A (en) * 1983-12-23 1985-02-19 Mcneil Roderick J Apparatus and method for material disposal
US4702073A (en) * 1986-03-10 1987-10-27 Melconian Jerry O Variable residence time vortex combustor
US4819571A (en) * 1986-08-08 1989-04-11 Eli-Eco Logic Inc. Process for the destruction of organic waste material
US5050511A (en) * 1986-08-08 1991-09-24 655901 Ontario Inc. Process for the destruction of organic waste material
US4954323A (en) * 1988-11-01 1990-09-04 The Standard Oil Company AOG incinerator NOx emission control via NH3 injection
US4934286A (en) * 1989-08-24 1990-06-19 Fowler Benjamin P Apparatus and method for the disposal of waste
US5817909A (en) * 1992-11-16 1998-10-06 Rhone-Poulenc Chimie Purification of waste/industrial effluents comprising organic/inorganic pollutants
US5704557A (en) * 1995-03-06 1998-01-06 Eli Eco Logic Inc. Method and apparatus for treatment of organic waste material
EP0773406A3 (en) * 1995-11-08 1997-12-10 Process Combustion Corporation Method to minimize chemically bound NOx in a combustion process
US20090000530A1 (en) * 2007-03-02 2009-01-01 Fujita Manufacturing Co., Ltd Waste oil combustion apparatus
US20100077942A1 (en) * 2008-09-26 2010-04-01 Air Products And Chemicals, Inc. Oxy/fuel combustion system with little or no excess oxygen
US20120012038A1 (en) * 2010-07-19 2012-01-19 Dylan Smuts Dual Chamber Combustor
US9611204B2 (en) * 2013-07-24 2017-04-04 Evonik Röhm Gmbh Method of regulating the water content in a continuous method for producing methacrolein
US20160159719A1 (en) * 2013-07-24 2016-06-09 Evonik Roehm Gmbh Method of regulating the water content in a continuous method for producing methacrolein
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GB2043854B (en) 1982-11-10
JPS622207B2 (enrdf_load_stackoverflow) 1987-01-19
GB2043854A (en) 1980-10-08
JPS55105111A (en) 1980-08-12
DE3004186A1 (de) 1980-08-21
DE3004186C2 (enrdf_load_stackoverflow) 1988-06-16
NL8000655A (nl) 1980-08-12

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